Fluid temperature control



y 20, 1952 G. A. TAYLOR 2,597,203

FLUID TEMPERATURE CONTROL v Filed Oct. 29, 1947 2 SHEETSSHEET 1 YIIIIIIIII'IIIIIIIIA 1 INVENTOR fly George A. Ely/or 72 ATTORNEY Patented May 20, 1952 FLUID-TEMPERATURE:CONTRLOL;

George A. Taylor, Eastiorang; N. J., assignm to:

N. J'., a'cor'porationpf NeWJersey Appl eation october w, 1947 ,wSerial-No. 182,776

s'clainiszrrcl. 1222481)}8 7 The. present invention relates to fiui d'trnper ature-control a'nd moreparticularlyto the construction and operation offiuid heat exchange 1 apparatus wherein .the temperature of fluid interiorly fof tubes is controlled. by regulating the new-6r heating :gasesexteriorly of the tubes.

l-leretofore, in A-heatexchange. apparatus ;uti1iz'- v mg. a gaseousmedium. exteriorly of tubes for I imparting heat to a gaseous fluid or vapor interiorly of the" tubes, numerousflue andtdamperl arrangements have been devised with aview to T maintaining more nearly. uniform vapor :outlet temperatures at varying loads. or -.capacities.'

However, suchefor'mfs of apparatus .in many in- I stances have-involved expensive and. complicated constructions and'furthermore do not-lendthem selves to application inthe simpler" formslof sup'erheater' boiler constructions; nor in existing superheater boiler installations.

An'object of myinventiomtherefore, is to pro-' vide a relatively. simple and inexpensiveform-of fluid-"temperature control apparatus app1icable,- forexar'nple, to a vapor generating I unit havingits vapor. superheating component formed of tubes in ithevpath of heating. gases from an as sociatedfurnace.

As: anadditiona-l'object it mypurpose to control the. temperature of superheated -vaporbyiproportioning the-flow of heating gasessover" difierent-portions of the heat transfen-surface within a common heating gas-pass.-

. Another object, in the operationsofa gas heated boiler -superheater-unit, is to :control super heated vapor; temperature-by imposing a-variablerestriction in av portiontof the pathzprovided for heating, gas flow under varying-load-conditions;'

A further object,- in the control of superheated vapor temperature undervarying load condi-w tion's, isto variably restrict heating .gas flow Y over a portion a of the vapor heating surface while maintaining substantiallyunrestricted heating gastflow over another portionn- A furtherrelated object is to control super-T heated. vapor temperature under --i-ncrea singload:

conditions 1 by. increasingly restricting heating-- asefi'ovv over a predetermined portion 2' of the vaporJ heating: surface. 1

A morespecificobject in the control of vapor superh'eattemperature is to regulateheating-gas fiow---by means-supported mainly on freelysuspendedvapor conducting-elements. I

The wariousfeatures of novelty which: characterize my invention are pointed out with parr ticulari-ty in the claims'zannexed to and forming a part of this specification; For :a' better-' understanding.-' 'of fth invention; its operating" gd: vantages. and specifi'c 'objectsf attained" b'yits use; reference. should -b'e'fhadl to the accompanying drawings and descriptive matterlin which IhaVe illustrated and described'a preferred emb'odiment of my. invention Of thfdrawings' Figl' l is a part y Fig ll3 is a 1 'gmentaryenlargement-hr Fig." 1 showing. details of'the" construction, including l a? representation "of wdarnperreleinents' in open and partly 'insec'tion; 'illustr'ating"a portionfof the damper-supporting structure as 'viewed"at line 4-4 of Fig; 3;rand

Figs. .5 and.16. aretransv'eise sections of the structureishown Fig.4, taken-i alongfline's 5 5 and 66 espectively.

heating gases discharging from anassociated fuel-fired furnace. TAs indicated-in'Fig'sfl and. the furnace includes a' primary chamber. l5 into which it may be assumed the fu'lis in'i tiallyl delivered, and anadjoining secondary f chamberlfi adapted 'to receive hot gases of com{ bustion' from the first namedi chamberl The- I 6 l are continuous furnace chambers-15. and I I across the width of the setting/between opposite fluid-cooled sidewalls] 'l,' but in the gas fi bw di rection; parallel to th'ose Walls, are separated by an upright dividing wall l8 formed;- at; least-V in ;part.rloy. a row' o'f tubes l having their upper ends connected. to :.boiler drum I3 and havingselected uppers endportions bent out from-the row to provide a screened-gas flow passage-"24 connecting-upper end- -portionsiof the chambers:

Anupright baffle' Wall 23,-extending downwardly from the upperfront drum 1 l3, terminates "in a lower edge portion 24 at an elevation slightly; above -theilower drums l5 and whorizohtally spaced relationship to the'. -1ower'dru!fr to definei 'ai' gasifiow -p'assa'ge-i-25 therebetween; -1- The =v\ha11?s2.3.

is formed mainly by a row of furnace wall tubes 26 having their upper ends connected to upper drum I3 and having upper end portions 27 fitted with suitable intertube closure means to provide a substantially continuous baffle wall structure. Wall tubes 2% are formed with horizontally inclined intermediate portions 28 which are arranged in screen formation and which extend forwardly and upwardly across the gas flow passage 25. The tube wall 23 constitutes a partition wall separating the upper part of chamber It, at one side, from a boiler tube space 29, at the opposite side. Gases entering the upper portion of chamber 16, through gas passage 2|, are directed downwardly therein to an enlarged lower portion wherein the direction of gas flow is reversed and the gases in turning around the lower end of partition 2! are caused to flow in a generally upward direction through the screened opening 25 into the tube space 29 which contains the main convection heated surface of the boiler-superheater unit, and from which gases are discharged through an upper gas outlet 3! extending substantially throughout the Width of the setting.

The boiler section, as shown, comprises a main tube bank 32 formed of horizontally spaced upright tubes 34 extending between and connected at opposite ends to the lower and upper drums l2 and 14, respectively. In the illustrated arrangement, where a relatively small number of other tubes 35, of larger diameter than tubes 34, and more widely spaced, are grouped at opposite ends of tube bank 32, upright bafilles 36 may be installed, inwardly from the respective side walls I 11, to block off the lower resistance gas flow path provided between the more widely spaced tubes of each group and thereby confine the major heating gas flow to the main bank of relatively closely spaced tubes 34. v

Tubes 3'! and 38, horizontally spaced in separate rows and connected at their opposite ends to boiler drums l2 and I3, are formed with vertically spaced lower end portions 39 and 4!, respectively, disposed above the screen tube formation 28 and extending forwardly at an upward inclination toward baiile wall 23. A bafile 42, supported on the tube row portion 4!, extends from a lower position adjacent to drum [2 to an upper position adjacent to and spaced from bafiie wall 23 so as to direct the major portion of heating gases from chamber l5 toward the front portion of tube space 29. Upper portions of tubes 31 and 38 are arranged upright, as shown, with the tube rows horizontally spaced from each other and from the upright baffle Wall 23. The front and rear upper drums l3 and M are connected by horizontally spaced circulating tubes 43 arranged, for example, in a plurality of rows and supporting a gas tight roof structure 45.

In the structure thus described, a space 43 is provided forwardly of the tube bank 32 for the accommodation of additional heat absorbing surface such as is afforded by a superheater 41, for example, of the multiple loop type, as indicated, and having tubes 48 arranged upright in successive tube coils or panels which are horizontally spaced throughout the width of the superheater space 46 between opposite side walls ll. As viewed in Fig. 1, the superheater tube coil assembly is suitably of greater extent vertically than horizontally, and of progressively increasing height toward its gas outlet end adjacent tube bank 32. In each coil or panel, successive tubes or tube lengths 48 are horizontally spaced and, being alternately connected by return bends 49 at opposite ends to form serially connected loops, provide a continuous fluid flow path from one end of the coil to the other. It is to be understood that adjacent tube loops and adjacent tube coils may be tied together in known manner at intervals throughout the height of the tube bank to'maintain adjacent tube lengths 48 inpredetermine d spaced relation, while permitting adequate tube length movement to accommodate relative expansion and contraction. A single slipjoint connector 5! is indicated in Fig. 3 as an example of the type suitable for tying together adjacent tube loops. Successive coils at their inlet and outlet ends are extended between circulating tubes as and through roof 45, and are connected to suitably supported inlet and outlet superheater headers 52 and 53 from which the entire superheater assembly is freely suspended. Inlet header 52 is connected to drum M by vapor inlet tubes 5 The superheater coils are proportioned in height so as to conform in general to the upper and lower boundaries of space 36 and thus, in the particular arrangement shown,- provide a relatively small clearance space 56 between the upper loop ends of the coils and the circulating tubes 43, and a similarly small clearance space 51 between the lower loop ends of the coils and the tube-supported baffle 42. The superheater coils, being disposed above bafile 42 and above the baffle-supporting tube row portion 41, are thus also vertically spaced from the lower drum [2.

In the operation of a unit such as disclosed, the hot gases entering space 29 from furnace chamber l3 are directed forwardly by baffle 42 so as to pass into the upper part of the space along the rearward side of the upright front wall 23 where resistance to gas flow is relatively low due to the relatively wide spacing of tube portions 37 and 38 in this region. The hot gases; due to their inertia, thus tend to rise to the uppermost part of space 29 with the result that'the gases are distributed substantially throughout the height of the space at its gas inlet end, thereby providing a continuous supply of hot gases substantially throughout the total gas inlet area of the adjacent superheater tube bank d1. The gases then follow a generally horizontal path through space 23, in contact with the superheater tubes of bank 47 and the boiler tubes of bank 32, and finally through gas outlet 3i.

A known characteristic of a convection heated superheater of this general type is that, with the heating gases continuously in contact with a fixed amount of superheating surface, the temperature of the superheated outlet vapor increases with increasing loads and decreases with decreasing loads, due to the accompanying changes in gas volume and temperature. Thus, in order to maintain a sufficiently high vapor outlet temperature under minimum load conditions, an amount of superheating surface might be required which under maximum load conditions would result in vapor outlet temperatures becoming undesirably high. My invention therefore contemplates positive control of vapor outlet temperature, under a wide range of load conditions, suitably by regulating the effectiveness of a predetermined portion or area of the superheating surface. In general, as loads are increased, it is my purpose to impose a restriction on gas fiow through a predetermined portion of the superheater space 45 and thereby reduce the proportion of heating gases flowing over a corresponding portion of the superheating surface, the

restriction'm gasefiowwin the present embodie ment,-: being-"limited to -a predetermined' upper portion of the space so as to permit'unrestrictedgas-.flow :through the remaining lower portionm By mak'ing the: restriction variable,-': the -proportioning of gas fiow OVer separate 'areas-Qf super-'2 heating surface may- :be adjusted accordance wit-hloadrconditions :to provide 1 the- -degreewof vapor xoutlet'atemperaturei"desired,1 within-alimits; determinedsbythe'particular design of unit; A";- form:- of .gas:=.;flow aproportioning; apparatus;:;: suitable fonz the? purpose described; is. indicated: lnfigeneralqin .iEig: 1,v and comprises: a damper mechanism-. 6! amounted rearwardly :xoisuperevi heaters 4-1 Siadjacent ithe :upper portion rthereofs: Theemechanismicfil is associated withz'xsuitably-a. arrangediwalhmeans: such i as a bafiles smiandn- 63. which:providezidefinitedelineation oft-la prede termineda gasz hut-let? area "or f'opening 51641:; with: respect :to which: the adamperr-mechanismiis"de signed .ttowtzoperatew It will be notedL-thaL-the upright upper refractory baffle; 62 extends. downev ;.-i wardly zfrom '.t-he1:roof= structure L 45 to a. position below the gupper ends. a of l-superheater tubes 1:48p; therebyi'defining the uppercmargintofxgas outlet area164 sand ;atw:the samefltime blocking. :ofi..the rearward end of .Lthe..- upper clearance space 5 6'. Theihafileiflgzwhich consists.:mainly.iof :moldable; ceramic;refractory material hardened in. place; may i-ncludeia flanged, metal platezportionlfid 3O posed along its lowenedge-andsecured by: U-bolts 6'! :to isuperheateritubesfifl .in the rearmostmow. That-lower; bafllezorrwallvfi3,.suitably. of a monolithiczrefractory. type, cxtendsacross superheater 1 tubes 48in a plurality'of'rows .in the"rearmostsection of the superheater tube;bank;thither" bafile -;6.3.being inclinedupwardly; in the downstream:gasrflow direction to definea gas1pass,,con.-;:. vergingztoward the. position of damper means 6 l Bafiieafifi ififlXtfiI'ldS from its lower :edgev 69- add acent: anzintermediate. row of the bank; and-terminates in-;.an nppenedge: H substantially, flush with the, downstreamg surfaces; of tubes. 68 to define; the lower-margin :of the: rectangular gas ;,o,ut1et areas; 64. 4. ,zThes'proyision :of .rbafiie' @163; inclined; in the: direction shown, rendersythepdamper means. 6| efiective over a greater height of the superheater tube bank 41 than is represented, by thezheight of t-he; damperedgas; dischargc areafifl. The ex-fl. 5 tentzoiheatgabsorbingsurface over which clamperz contra-ids refl ctive -is therefore r aterthan theibafiia were-omit ed; oriex ended. in :a plane. normalstc th zaxes of :the superheaterc-tubes;or;1; ped wd wnwa dly t ward 1: th wdamperc means: positi n-s; In.=. further detail, and referring; particularly to=.Eigs;,-2-6 inclusive, the damper element of the apparatus.tiS,v 0f the :multi-bladed-typehaving. b1a'des,-, '|2 operabletin unison, or separately, as desired; The damper-assembly extends. throughout the;.horizontal width of the gas outlet ,area, fifl-asfindicatedin Fig. 2, and damper blades 12, in;..closed-:position,"provide a substantially com- 3 pleteeclosurethroughout the vertical height of area slim -as indicated,- by the :brokenoutline: of. 85 blades-12 in.Fig-.-:= 3. Each blade," is,,d ivided;in length-,-into a suitable number of spaced-sections- 12,a,:-'l -2 b,c-12c,zfor example, to allowfor the ;rela-: tiveiamovement of adjacent portions-resulting, fromi-expansionv-andcontraction.

Thedampervassembly. 61 is supported solely on superheater tubes 68 forming therearmostrow; theqdamperiblades l2 being;supported at vertie callyrspacedglocatiom; and :eachlblade J2 being. separately@supportedcby;zmeansiof supports 1.1 355 6 whicmarcarrangedetc"permitangular movemen of the blade about a-piVotalaXis extendingntrans verselyof tubes ta adjacenttheirearwardisideio the row Each damperblade-H is supportedlatlz intervals along-its length, between dampen blade sections, "for exampley-as' detailed in Fig-164, and. also -adjacent' its ends-as indicated in Fig.2; :7

Each :support :13 comprises::abearing-1 lug bracket '14 having -its inner edgellconnected t a iitube 68 byi meanswf '-weld 'l5; =A rectangul'a notch- 16; formed inithe inneredgerof' each -1u 'ld and having itsiupper end openwis adapte to receive' a bar: 18', suitably formed in :sectiona lengths so'as to' maintain the\tubes 88. in sub stantiallyplanar alignment throughout the widt 2 of the rows The bar 18 which maybe continuous in length, or :in sectionsgis connected to"each: lug 14 by a weld- =19 'A notch 81 is formed in the -z. upper edge of each lug J l to receive; and support r a hollow -=trunnion member 8-2. the: baseot notch- 8| being :arcuate-- in' form to provide a suitable bearing surface.- The trunnion 82 is' retained in' notch 81 by means ofa narrow strap Stspannin'g I thenotch and secured --to the lug by-a weld-i84 :atleach-end.

Each damper blade-i2; or in the'specifidform shov'v-n', each -damper blade section, is secured to apipe or sleeve member 85 adapted to telescopewith-trunnion members 82 at oppositeends: The telescoped -ends-of parts 82 and 85- are separably' connected by bolts 86 -"extending' through; dia' metrically i positioned -pai=rs of holes 181. Each damper blade sectionincludes at least onestiff enerbar =89, mounted edgewise 'thereon and extending- =transverselylof the axis of rotationgeachbar 89 -being= secured-to a blade or-blad'e-section* by welded connectionsQ-I along-its inner contacting edge, and to thepipeor sleeve member b a" welded connection 9-2 at its inner-end; "It will be noted from-Figrfi that in order to control=gas;- flow--throughout the width of gas outlet 'area--64-,-'-- the-damper blade assembly necessarily -extends beyond the ends of the -rearmost -tube row*68.- In this construction each support 13 adjacent-one end i's' positionedintermediate the length; of an I end section 69aor Bile-*instead of between -sec--'-- tions,--and '-requi1'es-- a shortlength sleevemember" 93 and a corresponding stiffenerbar 89--t0 adequatel-y' support each outboard damper ;blade-por;- tionL- Each damper-"blade assembly, atone end,-in=-* eludes an extension shaft 94 suitably connectedto a sleeve length 93 at its inner end andterminatingw exteriorly of the adjacentsetting wall11in an outer end 1 portion to which; an "operating-crank arm-95 isrigidly: secured; ;As thus-arranged; any one-damper blade 12 may-be operatedseparately,-- and thus may be maintained open-or closed irre spective --of the-position of any other bladeor group-ofblades. If it is desired" to operate all damper-blades" in unison,-the crankgarms"95" may be interconnected by means of azlink'bar'9fii having a pivotal connection 91 with each cranki: arm 95-. Operationof the-group=of blades may 1 be effected-by means of" a lever'98' a-ffixed to-shaft 94 and having a chain 99, for example-, connectedthefeto-at-opposite ends;

A desirable feature of the 'disclosedarrange ment of temperaturecontrol apparatus is the" flexibility with which superheat temperatures, may be positively-controlled particularly at the higherscapacities; For example, in a vapor generating unithaving superheater surface arranged as shown,- and having arated capacity of- 350,000== lbs} ofasteam pep-houn the superheated -steame outlet temperatures, with damper 6| continuously open, could be expected to vary fromabout 850 F. at 70% rated capacity to about 890 F, at 100% rated capacity, an increase .of 40 F. for a 30% increase, in capacity. Under these conditions, gas flow is unrestricted throughout the entire superheater so as to render the total area of superheating surface effective, the vapor outlet temperature increasing with load due to the rising superheater characteristic. However, for the same capacity variation, with damper 6| continuously closed, the superheated steam outlet temperatures would range from about 820 F. at the 70% rating to about 870 F. at the 100% rating, an increase of 50 F. for the same increase in capacity. Under these last named con-, ditions, the maximum restriction is imposed on gas fiow through an upper portion of the superheater, while gas flow is unrestricted throughout all remaining portions. The result is a maximum reduction in the effectiveness of the upper superheater portion, and a consequent decrease insuperheat temperatures throughout the range, as compared with the first named conditions. It will be understood therefore, that by operating with the damper fully open at the specified lower capacity and fully closed at the specified higher capacity, the overall steam temperature variation is reduced to 20 F., with actual steam temperatures ranging from about 850 F. to 870 F. At intermediate capacities, the damper 6| would normally be adjusted to positions intermediate the fully-closed and fully-open positions, to provide varying degrees 'of gas flow restriction through the upper portion of the superheater, thereby varying the effectiveness of the upper superheater portion so as to maintain the gradation of superheat temperatures desired.

It is to be noted that under maximum load conditions, when the heating gases are at their highest temperatures, the gas flow controlling dampers 72 are in a closed or substantially closed position and lie in a plane parallel to the plane of the adjacent fluid cooled tubes 68 on which they are directly mounted. Du to the proximity of the tubes which are at substantially lower temperature, the damper elements are cooled by radiant heat transfer to the tubes, and accordingly are made of relatively light weight heat re- 1 sistant metal so that they may be mounted on the tubes, for adequate support thereby, and when mounted, may lie closely adjacent the tubes, for adequate heat transfer. Each blade 12, being formed of relatively thin metal plate, is adapted to be brought into contact with the adjacent tubes 68 substantially throughout its width when moved into closed position. Under lower load conditions, when gas flow and gas temperatures are lower, and dampers 12 are opened so as to increase the effectiveness of a greater extent of superheater surface, the heating gases which are thus permitted to flow over the controlled addi-.- tional superheater surface, and between the dampers, are at temperatures of low enough level to permit the dampers to be maintained without serious deterioration.

It is advantageous to position damper means 6| across the uppermost portion of the super: heater space 46 so as to make it effective with respect to the hotter gases which normally enter this region. Under low load conditions, when the dampers I2 are in open position, the gases flowing horizontally through the space tend to stratify, with the hotter gases forming the upper strata and enabling a higher superheat temperaoutlet temperatures at high loads.

tune to be maintained at low loads. As the. load is increased, and dampers 12 are moved toward the closed position, the restriction of gas flow is efiective with respect to the hotter strata so as to provide a lower increase in superheat temperature at increasing loads.

It will be further noted that, in the practice of my invention, the control of superheat is effected solely .by the regulation of suitably directed heating gas flow and thus obviates the need of special gas bypass conduits and dampers so often employed in prior art structures.

incorporated in existing boiler installations since no change in internal volume of the unit is required, nor any change in the amount of superheating surface. 7 With respect to the particular form of boiler unit herein illustrated, it is acknowedged that some of the heating gases, under high load conditions, might be caused :to pass curs, since the ultimate superheat temperature is continuously under positive control. of the specially arranged gas flow regulating means 6|, particularly as arranged with respect to the gas flow directing means 63.,

While in accordance with they rovisions of the statutes I have illustrated and described herein the best form of my invention now known to me, those skilled in the art. will understand that changes may be made in the form of the apparatus disclosed without departing from the spirit of the invention covered by my claims, and that certain features of my invention may sometimes be used to advantage without a corresponding use of other features.

I claim: a

1. In a superheated steam generator, a steam and water drum, steam generating tubes connected to discharge to said drum, means defining a horizontally extending single pass heating gas passage containing the major portions of said tubes and continuing to a gas outlet beyond said tubes, a superheater receiving steam from said drum and comprising a bank of spaced upright tubes extending across said passage in advance of said steam generating tubes, means supplying heating gases to said passage at the end forwardly of said bank, adjustable damper means supported on a row of said superheater tubes remote from said gas inlet end of said passage for effecting a superheat regulating restriction of the flow of the heating gases over end portions of tubes of said bank, said damper means having separately pivoted damper blade portions arranged to lie in a plane parallel to the axes of said supporting tubes, in contact with said supporting tubes, when rotated to a position of maximum flow restriction, and means for operating said damper blade portions from a location exteriorly of said passage at a side paralleling the flow of heating gases therethrough.

2. In combination with a superheater having its heating surface freely suspended within a gas flow pass through which heating gasesare F01 this reason, the invention may advantageously be e'r-adirectedq substantially horizontally in a single -*:pass'throughout the vertical; extent thereof, said -means; supported solely onelementsrof one of said rows for controlling the flow of saidsingle pass heating gases over said heating surface, said dampermeans comprising at least one damper blade having support means along one edge arranged-forpivotal blade movement about a horizontal axis, said damper blade support means :-:comprising brackets secured to tube lengths. in ---sa1d one row'of'elements, and relatively rigid :means supported bysaid brackets and engaging tube lengths of said row for-maintaining said engaged tube lengths substantially in alignment in the plane of said row.

3. In combination with a superheater having its heating surface freely suspended within a gas flow pass through which heating gases are directed substantially horizontally, said heating surface being provided mainly by tubular heat absorbing elements having upright tube length portions spaced apart in rows extending transversely of said heating gas flow, and damper means supported solely on elements of one of said rows for controlling the flow of heating gases over said heating surface, said damper means comprising damper blades having separate supports arranged for pivotal blade movement about vertically spaced horizontal axes, each of said damper blade supports comprising brackets having inner edge portions secured to tube lengths in the furthermost downstream row of said elements, horizontally axised trunnion members each received in and supported by one of said brackets, and tubular means integral with each of said damper blades and telescopingly received and supported by at least two of said trunnion members, said brackets having notches formed in their respective inner edge portions adjacent the tube lengths to which said brackets are secured and having a bar received in said notches for maintaining said tube lengths substantially in alignment in the plane of said row.

4. In combination with a superheater having its heating surface within a gas flow pass through which heating gases are directed substantially horizontally, said heating surface being provided mainly by tubular heat absorbing elements having upright tube length portions spaced apart in rows extending transversely of said heating gas flow, and damper means supported solely on elements of one of said rows for controlling the flow of heating gases over said heating surface, said damper means comprising damper blades at successive elevations having separate supports arranged for pivotal blade movement about vertically spaced horizontal axes, each of said damper blade supports comprising brackets secured to tube lengths in the furthermost downstream row of said elements, said damper blades in closed positions providing a space between blades at successive elevations, and means supported by brackets for one of said blades for closing said interblade space while restraining the respective bracket-supporting tube lengths against relative displacement.

5. In a vapor generator having vertically spaced drums comprising a lower drum and an upper drum, a bank of vapor generating tubes extending between and connecting said drums, means defining a heating gas passage containing :said', tube bank through which heatinggasesare -:caused q to l-fiow horizontally in a Sin le ,pass 1 throughout the total vertical cross sectional area .;of .said passage toan upper gas outlet downstream of said tube bank, asuperheater having i=the;major portion of its heating'surface formed of? tubes disposed within. said passage at 1an3up- "stream position relative to the position ofsaid itubebank, said superheater tubes being arranged in successive rows relative to the flow of said gases; damper means supported on superheater "tubes of'one of-sai-d rows forcontrolling the;fiow 'ofsaid gases over a predetermined upper portion of said heating surface, and means defining the gas :fiow area of said passage over'whichsaid damper means is effective comprising gazi baflle c-arranged intermediate the height of-said passage and sloping upwardly in a downstream direction across rows of said superheater tubes and terminating in an upper edge portion adjacent the lowermost portion of said damper means.

6. In a vapor generator having vertically spaced horizontally disposed drums including a lower drum and at least one upper drum, vapor generating tubes connecting said drums, means defining a single pass gas flow passage forwardly adjoining the vertical space between said drums and continuing throughout substantially the total height of said space to a gas outlet at the downstream side of said vapor generating tubes, means for directing gases substantially horizontally through said passage to said outlet, a superheater in the path of said gases having an upper portion of its vapor heating surface within an upper portion of said passage, means for conducting vapor to said superheater from said upper drum, and

E adjustable damper means controlling the flow of said gases through and from the upper portion of said passage and thereby over said upper portion of the vapor heating surface contained therein, said damper means extending downwardly from the upper boundary of said passage in overlapping relationship to said upper vapor heating surface portion at the downstream side thereof.

'7. In a superheated steam generator, a steam and water drum, steam generating tubes connected to discharge into said drum, means including said drum defining a horizontally extending single pass heating gas passage containing the major portions of said tubes and continuing to a gas outlet beyond said tubes, a superheater receiving steam from said drum and comprising a bank of spaced upright tubes extending across said passage in advance of said steam generating tubes, means supplying heating gases to said passage at the end forwardly of said bank, said steam generating tubes being displaced rearwardly from said superheater tubes to provide a gas receiving space between said generating tubes and superheating tubes, and adjustable damper means in said gas receiving space directly adjacent to and extending over a substantial portion of the height of a row of said superheater tubes remote from said gas inlet end of said passage for eflecting a superheatregulating restriction of the flow of the heating gases over end portions of tubes of said bank.

8. In combination with a superheater having its heating surface freely suspended within a gas flow passage through which heating gases are directed substantially horizontally in a single pass throughout the vertical extent thereof, said heating surface being provided mainly by tubular heat absorbing elements having upright tube length portions spaced apart in rows extending 11 transversely of said heating gas flow, damper means arranged directly adjacent to the furthermost downstream row of said superheater elements for controlling the flow of heating gases over said heating surface, and means defining a predetermined outlet area of said pass over which said damper means is effective comprising vertically spaced baflies arranged respectively above and below said damper means, said baflles including an upper upright baflie directly adjacent said furthermost downstream row and terminating downwardly in a lower edge portion marginally of said predetermined gas outlet area at said downstream row, said baflies including a lower horizontally inclined baflle arranged intermediate the height of said passage and extending across superheater tube length portions in a plurality of said rows and terminating at said furthermost downstream row in an upper edge portion marginally of said predetermined outlet area.

7 GEORGE A. TAYLOR. REFERENCES CITED The following references are oi record in the ,file of this patent:

UNITED STATES PATENTS 

